Development of kinetic model for CO hydrogenation reaction over supported Fe–Co

Development of kinetic model for CO hydrogenation reaction over supported Fe–Co–Mn catalyst

Published:2017 Issue:18 Volume:41 Page:10452-10466
ISSN:1144-0546
Container-title:New Journal of Chemistry
language:en
Short-container-title:New J. Chem.

Author:

Arsalanfar M.¹²³⁴^ORCID,Abdouss M.¹²³⁴,Mirzaei N.⁵⁶³⁴,Zamani Y.⁷⁸³⁴

Affiliation:

1. Department of Chemistry

2. Amirkabir University of Technology

3. Tehran

4. Iran

5. Department of Chemical and Petroleum Engineering

6. Sharif University of Technology

7. Research Institute of Petroleum Industry of the National Iranian Oil Company

8. Gas Research Division

Abstract

After determining CO consumption rate, the production rate of methane, paraffin, olefin and chain growth probability factor (α) was derived and described.

Publisher

Royal Society of Chemistry (RSC)

Subject

Materials Chemistry,General Chemistry,Catalysis

Link

http://pubs.rsc.org/en/content/articlepdf/2017/NJ/C6NJ04126D

Reference27 articles.

1. Water gas shift reaction kinetics in Fischer?Tropsch synthesis over an industrial Fe?Mn catalyst

2. The Fischer–Tropsch process: 1950–2000

3. Chain length dependent olefin re-adsorption model for Fischer–Tropsch synthesis over Co-Al2O3 catalyst

4. Preparation of steam activated carbon from black liquor by flue gas precipitation and its performance in hydrogen sulfide removal: Experimental and simulation works

5. Combustion characteristics and emissions of Fischer–Tropsch diesel fuels in IC engines

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